Methanotroph-based CH4 conversion technology is being widely studied due to its advantages of mild operating conditions and environmental friendliness. In this study, operating strategies were investigated for industrial CH4 sources in order to widely disseminate methanotroph-based CH4 conversion technology using the promising strain, Methylotuvimicrobium alcaliphilum 20Z. The optimal O2/CH4 ratio for extremely different CH4 concentrations was explored based on kinetic-based simulation for biological reaction, and experimentally proven using fermenter-scale experiments. As a result, when high CH4 concentration is used, ectoine production rate can be maximized (33.8 mg/L·h) at an O2/CH4 ratio of 1 while favoring the “production of metabolites”. On the other hand, in the low CH4 concentration case, when changing from the general O2/CH4 ratio of 4 to the optimal O2/CH4 ratio (i.e., 1), although the improvement in ectoine concentration was not noticeable (3.9 to 7.5 mg/L·h), the CH4 conversion rate rapidly decreased (50 to 20 %), suggesting that the focus in the low concentration case should be on “removal of CH4”. In the case of biogas, the rapid pH drop caused by the large amount of CO2 in the feed is offset by a buffer solution, and the concentration of Na+ ions increases during the overall reaction time. Therefore, the production of metaboiltes can be maximized while simultaneously controlling pH and Na+ ion through continuous operation with a high dilution rate (19.8 mg/L·h). Furthermore, major performance indicators for each industrial gas were derived through comprehensive comparative analysis, through which the “dual-functions” of methanotrophs could be emphasized. This study provides a practical and strategic approach for methanotrophs that can flexibly respond to diverse industrial CH4 sources.